download pdf version of PhD book - Universiteit Utrecht
download pdf version of PhD book - Universiteit Utrecht
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7.2 Network Generation<br />
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equations <strong>of</strong> mass balance. Under different saturation states, the flow equations<br />
are first solved and the resulting pore scale velocities are then used to simulate<br />
reactive solute transport.<br />
The main objective <strong>of</strong> this study is a better understanding <strong>of</strong> transport <strong>of</strong><br />
adsorptive/reactive solutes under unsaturated conditions. Although various<br />
mechanisms, such adsorption to the aws common line or moving AW interfaces<br />
have been suggested to affect the adsorptive transport, the exact role <strong>of</strong><br />
these processes are still unclear. In this study, adsorption over a wide range<br />
<strong>of</strong> saturations was considered by taking into account adsorption to both AW<br />
and SW interfaces. Regions <strong>of</strong> the pore space for which a wetting film <strong>of</strong> water<br />
coats the surface remain water-wet, as do the corners <strong>of</strong> the pore space<br />
where water still resides; however, we neglect adsorptive to interfaces associated<br />
with the water films. We have introduced a new formulation <strong>of</strong> adsorptive<br />
solute transport within a pore network which helps to capture the effect <strong>of</strong> limited<br />
mixing and adsorption under partially-saturated conditions. In contrast<br />
to former pore-network studies, which assign one (average) pressure and one<br />
(average) concentration to each pore element, we discretize an individual pore<br />
space into separate smaller domains, each with its own flow rate and solute<br />
concentration, in order to increase the accuracy <strong>of</strong> simulations. Thus, fluid<br />
fluxes along edges <strong>of</strong> each pore are calculated and taken into account in the<br />
simulation <strong>of</strong> adsorptive solute transport.<br />
In this paper, after construction <strong>of</strong> a Multi-Directional Pore-Network (MDPN)<br />
model, quasi-static drainage simulations are performed to determine pore-level<br />
distribution <strong>of</strong> each fluid phase. Then, steady-state flow is established and<br />
equations <strong>of</strong> mass balance for adsorptive solutes are solved to calculate transport<br />
properties <strong>of</strong> such a distribution and to obtain BTCs <strong>of</strong> solute concentration.<br />
Adsorption to both air-water (AW) and solid-water (SW) interfaces is<br />
modeled. These adsorption processes are independent <strong>of</strong> each other and each<br />
<strong>of</strong> them can have its own distribution coefficient and adsorbing area.<br />
7.2 Network Generation<br />
7.2.1 Pore size distributions<br />
In the present study, the pore structure is represented using a 3D MDPN<br />
model. Pore-body radii are assigned from a lognormal distribution, with no<br />
spatial correlation, explained in Section 6.2.<br />
Figure (7.1) shows the bore body size distribution used within the MDPN. Pore<br />
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